WORKING MIXTURE FOR REFRIGERATION EQUIPMENT

Abstract: The invention relates to refrigeration technology and can be used in low to medium temperature refrigeration equipment as well as in air conditioners and heat pumps. The proposed working mixture for refrigeration equipment contains octafluoropropane (C₃F₈) and sulphur hexafluoride (SF₆), as well as specific quantities of other components to allow the mixture to be used in refrigeration equipment operating under normal environmental conditions. The range within which are concentrated those components which preserve the azeotropic nature of the mixture, thereby reducing energy consumption, is identified. The proposed mixture can be used as a substitute for the ozone-damaging refrigerants of the F12, F22, F113 or other types, but does not require any fundamental modifications of or additions to the design of existing mass-produced refrigerators and air conditioners.

Description: The invention relates to refrigerating equipment and can be employed in low-temperature, medium-temperature and high-temperature refrigerating systems, as well as in air-conditioners and heat pumps. Technology Level There is known a working mixture for refrigerating systems which contains sulfur hexafluoride SF 6 and monochlorodifluoromethane CHClF 2 (USA Patent N 3642639, C 09 K 3/02, published in 1972). Cooling capability of this well-known mixture is higher than that of its individual components. The mixture can be applied with the greatest advantage in the field of low-temperature refrigerating systems in the range of boiling point T boil from -25 to -40°C. The drawback of the well-known mixture is that one of its constituents contains chlorine, which makes this mixture hazardous for the ozone layer. Ozone (O 3 ) is destroyed by chlorine (Cl) which is released from the fluorinechlorinecarbon compounds under the action of the hard solar radiation. There is known a working mixture for refrigerating systems which contains, mas. %: octafluoropropane (R 218) 35-80 and octafluorocyclobutane (R C318) 20-65. (USSR Inventor's Certificate N 1781279, C 09 K 5/00). The mixture is chosen as a prototype. This well-known working mixture is suited to the modern requirements of providing for safety of the ozone layer. The drawback of the well-known mixture for refrigerating systems is that the most effective from the standpoint of reducing power consumption range of concentrations of its constituents determines high boiling temperature of the mixture, which does not allow to use the mixture in household and industrial low-temperature and medium-temperature refrigerators. For the most effective concentration R 218/R C318 equal to 40/60, boiling temperature is -19°C, and for proportion 35/65 it is -22°C. Essence of the Invention The purpose of the invention is to extend the temperature range in which a mixture based on octafluoropropane can be used, to reduce power consumed when using refrigerating equipment, and to provide for the safety of the ozone layer. To achieve the above purpose there is proposed a working mixture for refrigerating systems which contains octafluoropropane (C 3 F 8 ) and sulfur hexafluoride (SF 6 ). The constituents' content in mass % is as follows: C 3 F 8 36 - 99.9 SF 6 0.1 - 64 Besides, the constituents' content in mass % is as follows The distinction of the proposed mixture resides in its composition and proportion of the constituents. Sulfur hexafluoride SF 6 possesses limitless solubility in octafluoropropane (C 3 F 8 ), has rather low boiling temperature, exquisitely stable, nonflammable. The peculiarity of SF 6 from the standpoint of reducing the cycle power consumption is the low index of its adiabat (1.02 - 1.04). Not the least of the factors is relatively low cost of sulfur hexafluoride (at least half as much as the cost of R218 or RC318). The proposed mixture can be used both in the form of azeotropic composition, in particular when the proportion of constituents C 3 F 8 - SF 6 in mas. % is 4.5 : 95.5, and in the form of unazeotropic mixture, when the constituents' contents is beyond the azeotropic region. The existence of azeotropic region is established in an experiment as follows from the data provided below. The mixture of C 3 F 8 and SF 6 taken in amount of 1 kg with a proportion of its constituents by mass 4/96 when subjected to slow evaporation retained its composition in a liquid phase at the liquid phase depletion down to 0.05 kg with accuracy of up to 0.1 mas.%. Before it is charged into a refrigerating system, the mixture is prepared in an isolated cylinder - filling tank by the weight method with the control over the mixture composition. The table presents calculated and experimental data obtained in the research. Composition mas.% Boiling t° (C) at p=1 atm. Critical t° (C) Power consumption at condensation t=20°C, Wt 0.3 SF 6 - 37 72 127 99.7 C 3 F 8 4 SF 6 - 38 72 102 96 C 3 F 8 60 SF 6 - 45 55 142 40 C 3 F 8 As follows from the data of the above table, in the range of constituents' concentrations around 4 mas.% SF 6 power consumption is reduced. Incorporation of SF 6 into the mixture at the same time allows to extend the temperature range for employment of the working mixture to include low-temperature region. Besides, the proposed working mixture is ecologically clean (safe for the ozone layer), because the molecule of SF 6 does not contain Cl atoms, and the gas of sulfur hexafluoride is used in medicine as a medium which is safe for a man. Important features of the proposed working mixture are its high stability, non-flammability, non-explosiveness, corrosion indifference. Boundary values of concentrations of the working mixture constituents are determined, on the one hand, by minimum SF 6 concentration in the mixture, at which the effect of reduction in power consumption is reliably retained (0.1 mas.%), and on the other hand - by the mixture critical temperature, which shall not be below + 55°C, i.e. condensation temperature accepted for medium-temperature and high-temperature compressors of refrigerating systems. An increase in the SF 6 concentration above 64 mas.% leads to a drop in the mixture critical temperature, which in its turn interferes with the cycle in a refrigerating system, operating under the normal ambient conditions, because in such conditions the excessive SF 6 concentration will prevent the mixture from condensation, and, therefore, cold will not be generated. Thus, the proposed working mixture can find application in low-temperature, medium-temperature and high-temperature refrigerating systems, in air-conditioners and heat pumps. And due to the above-mentioned features the proposed working mixture allows the change-over of the refrigerating equipment, currently based on the ozone layer damaging refrigerants (R-12, R-22, R-113, R-114 and so on) to the proposed mixture, and with such change-over it is not required to modify and amend designs of the serial refrigerators and air-conditioners, as well as to develop new oils, rubbers and structural materials.

Claims: Working mixture for refrigerating systems, which contains octafluoropropane (C 3 F 8 ) and sulfur hexafluoride (SF 6 ). Working mixture for refrigerating systems according to Claim 1, distinguished by the following components' contents in the mixture in mas.%: Octafluoropropane 36 - 99.9 Sulfur hexafluoride 0.1 - 64 Working mixture for refrigerating systems according to Claim 1 distinguished by the following components' content in mas.%: Octafluoropropane 95 - 97 Sulfur hexafluoride 3 - 5

Inventors: MAZURIN IGOR MIKHAILOVICH, MAZURIN, IGOR MIKHAILOVICH
Applicants: COOPERATIVE ELEGAZ, COOPERATIVE "ELEGAZ"
Application year: 1994
Main classification: C09K5
IPC codes: C09K5